US1205007A - Process of treating lignite. - Google Patents

Process of treating lignite. Download PDF

Info

Publication number
US1205007A
US1205007A US341415A US341415A US1205007A US 1205007 A US1205007 A US 1205007A US 341415 A US341415 A US 341415A US 341415 A US341415 A US 341415A US 1205007 A US1205007 A US 1205007A
Authority
US
United States
Prior art keywords
water
lignites
heating
treated
treating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US341415A
Inventor
Camillo Melhardt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US341415A priority Critical patent/US1205007A/en
Application granted granted Critical
Publication of US1205007A publication Critical patent/US1205007A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00Treating solid fuels to improve their combustion
    • C10L9/08Treating solid fuels to improve their combustion by heat treatments, e.g. calcining

Definitions

  • the before mentioned combinations contain, for example, succin-imid or the like, and under certain temperatures which cannot effect a dry distillation of the entire material, they are caused to burst by the escaping gases which are driven off under heat (such as carbon dioxid and carbon monoxid) and thereby lose the capaciiz of subsequently taking up again water om the atmosphere.
  • bitumen which is thus set free is brought to its natural melting point and, on account of its finely divided condition, especially in the case of pure li ite, closes the numerous pores which won (1 otherwise serve to-absorb the water.
  • the resent invention relates to a prom for utilizing the qualities of the materials under consideration for obtaining a confin Specification of Letters Patent.
  • An object of my invention is to provide a process by means of which the specific gravlty of the llgnlte can be lessened, thereby permitting the ready separation of the lignite from the associated foreign matter perature, when, according to the kind and I quantity of the combinations under treatment, a temperature from 180-250 degrees centigrade is allowed to act for a suflicient period of time (8-10 hours) on the previously dried material, and in closed vessels permitting the gases to escape.
  • the heating period as well as the height of temperature are very essential. A change of the combinations at the indicated temperatures can in most cases only be realized after several hours. Essentially the lower temperatures do not result in, even after alonger period of time, a complete decomposition of the ester.
  • the lignites, brown coal, or other materials which enter into consideration for this process, are naturally of lighter specific weight, float on water, and are difiicult to he,
  • the calorific efiect of the material thustreated amounts according to the raw 'muterial to be treated, to 60007500 calories, the valuable heating elements being retained.
  • Example II The material is treated in the same way as described in the foregoing example, only electrical energy is used as a source of heat.
  • Example III Wet brown coal intermixed with well preserved pieces of wood is, on accountfof its great amount of resins, the
  • a liquid medium heavier than water such as a salt solution of 1-2 1%. strength.
  • the fuel materials treated according to I and II examples are placed immediately after leaving the heating vessels, into water or strongly diluted salt solutions and the other matters which sink to the bottom are drawn off in the customary manner of coal washing.
  • I claim 1 The herein described pose of increasing their, calorific efiect and their permanent dephlegmation,-which consists in heating the material in a closed vessel with outlet to drive ofl certain of the gases and all of the water, and maintaining the temperature sufliciently low and in such a duration to prevent the decomposition of the remaining heat giving elements capable of decomposition, and separating out the ashy portions of the treated material.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Description

UNITED STATES PATENT OFFICE.
oamnno mnnnannnor srarmnnne mumcn, GERMANY.
PROCESS OF TREATING LIGNITE.
1T0 Drawing.
To all whom it may concern:
Be it known that I, GAMILLO MELHARDT, subject'of the German Emperor, residing at Starnberg-Munich, Germany, have invented certain new and useful Improvements in Processes of Treating Lignites, of which the following is a specification.
It has been found that pure lignites or such materials which are strongly intermingled with them, as for exam le, brown coal, peat, or the like, ofier consi erable resistance to briqueting, whereas this is not the case with brown coal in lumps. The briquets produced from lignites do not possess sufiicient compactness and when stored away absorb moisture. Beside these disadvantages of physical nature which make the briqueting of lignites and the like a failure, there are also chemical objections regarding the unfitness of the said materials for briqueting pur oses. It has been found that bitumen, Whic is indispensable for obtaining good briqueting results, is not contained in the cited raw materials in a free condition, but only in very complicated combinations, in most cases esters or imides. Such combinations cannot, however, be melted nor deprived of their water at that temperature which is technically admissible for bri ueting. They absorb water, which causes t e briquet to burst after it has left the press in apparently solid condition.
According to the origin of the respective raw mater1al,'the before mentioned combinations contain, for example, succin-imid or the like, and under certain temperatures which cannot effect a dry distillation of the entire material, they are caused to burst by the escaping gases which are driven off under heat (such as carbon dioxid and carbon monoxid) and thereby lose the capaciiz of subsequently taking up again water om the atmosphere.
The reason for this is that the bitumen which is thus set free is brought to its natural melting point and, on account of its finely divided condition, especially in the case of pure li ite, closes the numerous pores which won (1 otherwise serve to-absorb the water.
The resent invention relates to a prom for utilizing the qualities of the materials under consideration for obtaining a confin Specification of Letters Patent.
Patented Nov. 14, 1916.
Application filed January 20, 1915. Serial N0. 3,414.
An object of my invention is to provide a process by means of which the specific gravlty of the llgnlte can be lessened, thereby permitting the ready separation of the lignite from the associated foreign matter perature, when, according to the kind and I quantity of the combinations under treatment, a temperature from 180-250 degrees centigrade is allowed to act for a suflicient period of time (8-10 hours) on the previously dried material, and in closed vessels permitting the gases to escape.
The heating period as well as the height of temperature are very essential. A change of the combinations at the indicated temperatures can in most cases only be realized after several hours. Essentially the lower temperatures do not result in, even after alonger period of time, a complete decomposition of the ester.
The lignites, brown coal, or other materials which enter into consideration for this process, are naturally of lighter specific weight, float on water, and are difiicult to he,
ously dried and then heated to a temperature of 180-250 degrees centigrade, in closed vessels permitting the gas to escape. The heating is to be continued as long as watervapors andnon-condensed gas, as for example, carbonic acid, are being driven ofi. From eight to ten hours will generally be required. The loss of gas and water driven off, will amount to 15-20% after complete drying. The material is cooled in. any known manner, and is ready for use, if the impurities, the ashy portions, do not exist.
The calorific efiect of the material thustreated amounts according to the raw 'muterial to be treated, to 60007500 calories, the valuable heating elements being retained. Example II: The material is treated in the same way as described in the foregoing example, only electrical energy is used as a source of heat.
Example III: Wet brown coal intermixed with well preserved pieces of wood is, on accountfof its great amount of resins, the
most valuable one and often erroneously termed lignite but contains great uantities .of other matters, which considera ly raise the ash content of this fuel and therefore .make important coal mines unprofitable. A
on a liquid medium heavier than water, such as a salt solution of 1-2 1%. strength.
The fuel materials treated according to I and II examples, are placed immediately after leaving the heating vessels, into water or strongly diluted salt solutions and the other matters which sink to the bottom are drawn off in the customary manner of coal washing.
I claim 1. The herein described pose of increasing their, calorific efiect and their permanent dephlegmation,-which consists in heating the material in a closed vessel with outlet to drive ofl certain of the gases and all of the water, and maintaining the temperature sufliciently low and in such a duration to prevent the decomposition of the remaining heat giving elements capable of decomposition, and separating out the ashy portions of the treated material.
2. The herein described method of treatmethod of treat- .ing lignites, peat,-and-the like for the puring lignites, peat, and the like for the purpose of increasing their calorific effect and their permanent dephlegmation, which consists in heating the material in a closed vessel with outlet to drive off certain of the gasesand all of the water, maintaining the temperature sufliciently low and in such a duration to prevent the decomposition of the remaining heat giving elements capable of decomposition and separating out the ashy portions of the treated material by subjecting thematerial to a sifting action in Water or a salt solution. I
3. The herein described method of treating lignites and the like, which consists in drying the same, heating the material in a closed vessel until all the water and certain of the gases have been driven off and the y bitumen has been set free, and subsequently separating the material thus treated from the heavier foreign matter.
4:. The herein described method of treating lignites and the like, which consists in drying the same, heating the material in a closed vessel until all'the water and certain of the gases have been driven 011' and the bitumen set free, and subsequentlv separating the lighter treated material from the heavier material accompanying it by floating the same on a liquid medium of greater specific gravity than the treated material and of less specific gravity than the foreign matter.
5. The herein described method of treatinghgnites and the like, which consists in drying the same, heating the material in a closed vessel until all of the water and certain of the gases have been driven off and the bitumen has been'set free, and subse-- quently separating the lighter treated material-from the heavier material accompany ing it by floating the same on asalt solution. In-test1mony whereof I have affixed my signature in presence of two witnesses.
CAMILLO MELDT.
Witnesses:
N. Roman, ARTHUR Guns.
US341415A 1915-01-20 1915-01-20 Process of treating lignite. Expired - Lifetime US1205007A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US341415A US1205007A (en) 1915-01-20 1915-01-20 Process of treating lignite.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US341415A US1205007A (en) 1915-01-20 1915-01-20 Process of treating lignite.

Publications (1)

Publication Number Publication Date
US1205007A true US1205007A (en) 1916-11-14

Family

ID=3272935

Family Applications (1)

Application Number Title Priority Date Filing Date
US341415A Expired - Lifetime US1205007A (en) 1915-01-20 1915-01-20 Process of treating lignite.

Country Status (1)

Country Link
US (1) US1205007A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2700554A1 (en) * 1976-01-12 1977-07-14 Edward Koppelman PROCESS FOR PROCESSING LIGNITE-LIKE COAL AS FUEL

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2700554A1 (en) * 1976-01-12 1977-07-14 Edward Koppelman PROCESS FOR PROCESSING LIGNITE-LIKE COAL AS FUEL

Similar Documents

Publication Publication Date Title
US2717868A (en) Desulfurization of low temperature carbonization char
US1158364A (en) Process of making cohering masses.
US1205007A (en) Process of treating lignite.
US1503304A (en) Briquetting
US3093463A (en) Smokeless briquettes
US4188191A (en) Process for reducing the sulfur content of coal and coal char and the ignition temperature of coal char
US1564142A (en) Utilizing sulphite cellulose lye
US1000479A (en) Briquet and method of making the same.
US3026252A (en) Method of producing a carbonaceous product from low grade coal
US1116024A (en) Method of briqueting iron ores and the like.
US1233144A (en) Smelting process.
US1189254A (en) Production of aluminates from alunite.
US1353532A (en) Producing compounds of radium
US701365A (en) Briquet and method or process of producing same.
US2463204A (en) Recovery of sludge acids
US1380195A (en) Process of making potash
US2040609A (en) Briquetted fuel and process of making
US1609498A (en) Cooling of fuel briquettes
US711380A (en) Process of manufacturing a solid combustible from petroleum, sulfuric acid, and lime.
US1619649A (en) of london
US624629A (en) Archibald a
US1038370A (en) Process for briqueting flue-dust and the article of manufacture produced thereby.
US1154980A (en) Process for the manufacture of agglomerates.
US1416546A (en) Utilizing coal slimes
US1664998A (en) Process of manufacturing fuel briquettes